CN1065578C - Pulp bleaching - Google Patents

Pulp bleaching Download PDF

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Publication number
CN1065578C
CN1065578C CN95194782A CN95194782A CN1065578C CN 1065578 C CN1065578 C CN 1065578C CN 95194782 A CN95194782 A CN 95194782A CN 95194782 A CN95194782 A CN 95194782A CN 1065578 C CN1065578 C CN 1065578C
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CN
China
Prior art keywords
chlorine dioxide
stage
bleaching
slurry
chelating agent
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Expired - Fee Related
Application number
CN95194782A
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Chinese (zh)
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CN1157644A (en
Inventor
M·达尔
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Valmet AB
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Sunds Defibrator Industries AB
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/1026Other features in bleaching processes
    • D21C9/1042Use of chelating agents
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/12Bleaching ; Apparatus therefor with halogens or halogen-containing compounds
    • D21C9/14Bleaching ; Apparatus therefor with halogens or halogen-containing compounds with ClO2 or chlorites
    • D21C9/144Bleaching ; Apparatus therefor with halogens or halogen-containing compounds with ClO2 or chlorites with ClO2/Cl2 and other bleaching agents in a multistage process
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/16Bleaching ; Apparatus therefor with per compounds
    • D21C9/163Bleaching ; Apparatus therefor with per compounds with peroxides

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Paper (AREA)
  • Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
  • Detergent Compositions (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Medicinal Preparation (AREA)
  • Coils Or Transformers For Communication (AREA)
  • Semiconductor Lasers (AREA)
  • Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)

Abstract

Bleaching of chemical pulp in several steps comprising final bleaching with chlorine dioxide and, respectively, hydrogenperoxide. The pulp is treated directly in connection to the chlorine dioxide step (3) without intermediate washing with chelating agent (2) for the elimination of metal ions, preferably manganese. The pulp is thereafter washed (4) and bleached with hydrogenperoxide (5).

Description

The bleaching of slurry
The present invention relates to bleaching with chemical sizwe form lignocellulosic material.More particularly, the present invention relates to last bleaching to slurry by adopting chlorine dioxide and hydrogen peroxide to carry out as bleaching agent.
In order to carry out peroxide bleaching effectively, slurry must be removed particularly manganese ion of metal ion haply.Metal ion comes out as a result of this stage condition is dissolved in chlorine dioxide stage usually, is removed in the washing stage thereafter then, after this can carry out peroxide bleaching to slurry.This in most of the cases is enough to expend volume production with rational peroxide and gives birth to gratifying ISO lightness.
Have now found that, might further reduce the metal ion content in the slurry, thereby reduce the peroxide amount of expending and/or increase the ISO lightness.According to the present invention, this is by adopting the processing that chelating agent carries out with chlorine dioxide stage directly links to each other to realize to slurry.
Characteristics of the present invention can be apparent from claims.
Accompanying drawing below with reference to two embodiment of the present invention specifically describes the present invention.
Fig. 1 and 2 represents two examples of layout figure of the present invention.
Bleaching process comprises some bleaching stages, and wherein last bleaching is that separately the stage carries out for by chlorine dioxide and peroxide two.
In the embodiment in figure 1, slurry is at first being handled (the Q stage) 2 by chelating agent after a washing stage 1 in advance, by chlorine dioxide treatment (D stage), add this two kinds of chemicalss successively in these two stages then.After the D stage 3, slurry was washed in the washing stage 4, and bleach (the P stage) 5 by hydrogen peroxide, wash once more in the washing stage 6 then.According to another embodiment of Fig. 2, D in the stage chlorine dioxide feed in raw material on order prior to the chelating agent in the Q stage 2.In other respects, all the embodiment with Fig. 1 is suitable for this embodiment.
Therefore, importantly, carry out chlorine dioxide and chelating agent successively reinforced promptly be not to add together simultaneously but directly link to each other, do not carry out any washing therebetween.Found that chelating agent will produce ill effect with chlorine dioxide, adding then can produce aforementioned effect successively.Therefore, the present invention comprises a kind of improved bleaching process, and wherein bleaching agent, especially hydrogen peroxide can more effectively be used.
Q stage and the condition of D in the stage can be standards.This comprises the stage for Q: the slurry enrichment factor is 1-20%, is preferably 8-15%; Temperature is 45-100 ℃, is preferably 70-90 ℃; The pH value is 1.5-8, is preferably 2-4; Time is 10-120 minute, is preferably 10-60 minute.To subsequently P stage also can with other add or not in addition the traditional approach of oxygen carry out.But as mentioned above,, can reduce the reinforced or increase ISO lightness of peroxide as a result according to process of the present invention.So in fact, make peroxide obtain more efficient use.
Certainly, the present invention has more than and is limited to described embodiment, and can change in design scope of the present invention.

Claims (3)

1. method with some stage bleaching chemical sizwes, comprise the last bleaching of adopting chlorine dioxide and hydrogen peroxide respectively, it is characterized in that, for institute/stating slurry employing chelating agent (2) carries out directly linking to each other with chlorine dioxide stage (3) and not having middle processing 10-120 minute of washing, to eliminate especially manganese ion of metal ion, then described slurry is washed (4) and adopts hydrogen peroxide to bleach (5).
2. the method for claim 1 is characterized in that, directly adopts chelating agent (2) that described slurry is handled before in described chlorine dioxide stage (3).
3. the method for claim 1 is characterized in that, directly adopts chelating agent (2) that described slurry is handled afterwards in described chlorine dioxide stage (3).
CN95194782A 1994-08-31 1995-08-11 Pulp bleaching Expired - Fee Related CN1065578C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
SE9402885A SE514697C2 (en) 1994-08-31 1994-08-31 Elimination of metal ions in pulp bleaching
SE94028859 1994-08-31
SE9402885-9 1994-08-31

Publications (2)

Publication Number Publication Date
CN1157644A CN1157644A (en) 1997-08-20
CN1065578C true CN1065578C (en) 2001-05-09

Family

ID=20395066

Family Applications (1)

Application Number Title Priority Date Filing Date
CN95194782A Expired - Fee Related CN1065578C (en) 1994-08-31 1995-08-11 Pulp bleaching

Country Status (17)

Country Link
US (1) US6540872B1 (en)
EP (1) EP0778909B1 (en)
JP (1) JPH10505639A (en)
CN (1) CN1065578C (en)
AT (1) ATE226658T1 (en)
AU (1) AU687626B2 (en)
BR (1) BR9508653A (en)
CA (1) CA2197771A1 (en)
DE (1) DE69528660T2 (en)
ES (1) ES2185715T3 (en)
FI (1) FI970821A0 (en)
NO (1) NO970907D0 (en)
NZ (1) NZ292288A (en)
PT (1) PT778909E (en)
SE (1) SE514697C2 (en)
WO (1) WO1996006976A1 (en)
ZA (1) ZA957070B (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6375797B1 (en) * 1996-06-20 2002-04-23 Andritz-Ahlstrom Oy Bleaching chemical pulp in a PkDQ-Po Sequence
SE507742C2 (en) * 1996-11-08 1998-07-06 Sunds Defibrator Ind Ab Bleaching of pulp with chlorine dioxide, alkali and complexing agents without intermediate washes
SE0200981D0 (en) * 2002-03-28 2002-03-28 Eka Chemicals Ab Process for bleaching lignocellulose-containing non-wood pulp
JP4513959B2 (en) * 2004-09-17 2010-07-28 三菱瓦斯化学株式会社 Semi-bleaching bleaching process for chemical pulp for papermaking
FI123102B (en) 2006-03-31 2012-11-15 Laennen Tutkimus Western Res Inc Oy Chemical pulp bleaching process
PT2288752E (en) 2008-06-20 2014-05-07 Int Paper Co Composition and recording sheet with improved optical properties
CN101812812B (en) * 2009-02-25 2012-08-08 山东福荫造纸环保科技有限公司 Elemental chlorine free bleaching method for plant fiber stuff

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2219504B1 (en) * 1972-04-21 1974-02-28 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt MULTI-STAGE BLEACHING OF PULP WITH SIGNIFICANTLY REDUCED CHLORINE USE
WO1991011554A1 (en) * 1990-01-31 1991-08-08 Eka Nobel Ab Process for bleaching of ligno-cellulosic material
US5091054A (en) * 1989-08-18 1992-02-25 Degussa Corporation Process for bleaching and delignification of lignocellulosic
WO1993014262A1 (en) * 1992-01-21 1993-07-22 Sunds Defibrator Industries Aktiebolag Bleaching of chemical pulp

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1100709A (en) * 1965-06-25 1968-01-24 Pulp Paper Res Inst Two-stage purification of fibrous cellulose material
EP0402335B2 (en) * 1989-06-06 2001-03-14 Eka Chemicals AB Process for bleaching lignocellulose-containing pulps
SE500616C2 (en) * 1993-06-08 1994-07-25 Kvaerner Pulping Tech Bleaching of chemical pulp with peroxide at overpressure
SE502706E (en) * 1994-04-05 1999-09-27 Mo Och Domsjoe Ab Preparation of bleached cellulose pulp by bleaching with chlorine dioxide and treatment of complexing agents in the same step

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2219504B1 (en) * 1972-04-21 1974-02-28 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt MULTI-STAGE BLEACHING OF PULP WITH SIGNIFICANTLY REDUCED CHLORINE USE
US5091054A (en) * 1989-08-18 1992-02-25 Degussa Corporation Process for bleaching and delignification of lignocellulosic
WO1991011554A1 (en) * 1990-01-31 1991-08-08 Eka Nobel Ab Process for bleaching of ligno-cellulosic material
WO1993014262A1 (en) * 1992-01-21 1993-07-22 Sunds Defibrator Industries Aktiebolag Bleaching of chemical pulp

Also Published As

Publication number Publication date
DE69528660D1 (en) 2002-11-28
US6540872B1 (en) 2003-04-01
PT778909E (en) 2003-01-31
JPH10505639A (en) 1998-06-02
ZA957070B (en) 1996-04-15
NO970907L (en) 1997-02-27
EP0778909A1 (en) 1997-06-18
DE69528660T2 (en) 2003-06-26
ES2185715T3 (en) 2003-05-01
SE514697C2 (en) 2001-04-02
FI970821A (en) 1997-02-27
FI970821A0 (en) 1997-02-27
NZ292288A (en) 1997-11-24
AU687626B2 (en) 1998-02-26
NO970907D0 (en) 1997-02-27
CN1157644A (en) 1997-08-20
SE9402885L (en) 1996-03-01
ATE226658T1 (en) 2002-11-15
WO1996006976A1 (en) 1996-03-07
BR9508653A (en) 1997-11-11
AU3401795A (en) 1996-03-22
EP0778909B1 (en) 2002-10-23
SE9402885D0 (en) 1994-08-31
CA2197771A1 (en) 1996-03-07

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